US9422394B2

US9422394B2 - Thermoplastic polyurethane and associated method and article

Info

Publication number: US9422394B2
Application number: US13/929,961
Authority: US
Inventors: Edward Norman Peters
Original assignee: SABIC Global Technologies BV
Current assignee: SHPP Global Technologies BV
Priority date: 2013-06-28
Filing date: 2013-06-28
Publication date: 2016-08-23
Also published as: KR102049356B1; JP2016524023A; EP3013884B1; CN105283482B; KR20160027089A; EP3013884A4; CN105283482A; WO2014209934A1; JP6096989B2; EP3013884A1; US20150004341A1

Abstract

A thermoplastic polyurethane is formed by the reaction of a specific hydroxy-diterminated poly(phenylene ether) and an organic diisocyanate. The polyurethane-forming reaction optionally employs diols other than the hydroxy-diterminated poly(phenylene ether). Compared to thermoplastic polyurethanes lacking the residue of the hydroxy-diterminated poly(phenylene ether), the thermoplastic polyurethanes described herein exhibit properties including one or more of improved heat and oxidation resistance, improved resistance to acids, bases, and solvent, and reduced water absorption.

Description

BACKGROUND OF THE INVENTION

Thermoplastic polyurethanes (TPUs) are prepared from diols and diisocyanates. See, e.g., D. Randall and S. Lee, “The Polyurethanes Book”, New York: John Wiley & Sons, 2003; and K. Uhlig, “Discovering Polyurethanes”, New York: Hanser Gardner, 1999. The isocyanate groups of the diisocyanate react with the hydroxyl groups on the diol to form a urethane linkage. The diol can be, for example, a low molecular weight polyether diol or polyester diol. The diisocyanate can be aliphatic or aromatic. The family of TPU resins is very complex because of the enormous variation in the compositional features of the diols and diisocyanates. This variety results in a large numbers of polymer structures and performance profiles. Indeed, TPUs can be rigid solids, or soft and elastomeric. TPUs are fully thermoplastic and can be melt-processed.

The generally recognized useful features of TPUs include high impact strength even at low temperatures, good abrasion resistance, good heat resistance, excellent resistance to non-polar solvents and fuels and oils, resistance to ozone and oxidation and humidity, and good electrical resistance. Less desirable features include high moisture absorption and lower rigidity at elevated temperatures.

There exists an opportunity for TPUs that exhibit improvements in one or more of reduced moisture absorption, increased heat resistance, and increased strength at high elongation.

BRIEF DESCRIPTION OF THE INVENTION

One embodiment is a thermoplastic polyurethane comprising: a plurality of poly(phenylene ether) repeat units having the structure

wherein each occurrence of Q¹is independently halogen, C₁-C₁₂hydrocarbylthio, C₁-C₁₂hydrocarbyloxy, C₂-C₁₂halohydrocarbyloxy wherein at least two carbon atoms separate the halogen and oxygen atoms, or unsubstituted or substituted C₁-C₁₂hydrocarbyl provided that the hydrocarbyl group is not tertiary hydrocarbyl; each occurrence of Q²is independently hydrogen, halogen, C₁-C₁₂hydrocarbylthio, C₁-C₁₂hydrocarbyloxy, C₂-C₁₂halohydrocarbyloxy wherein at least two carbon atoms separate the halogen and oxygen atoms, or unsubstituted or substituted C₁-C₁₂hydrocarbyl provided that the hydrocarbyl group is not tertiary hydrocarbyl; each occurrence of R¹and R²is independently hydrogen, halogen, C₁-C₁₂hydrocarbylthio, C₁-C₁₂hydrocarbyloxy, C₂-C₁₂halohydrocarbyloxy wherein at least two carbon atoms separate the halogen and oxygen atoms, or unsubstituted or substituted C₁-C₁₂hydrocarbyl provided that the hydrocarbyl group is not tertiary hydrocarbyl; m and n are independently 0 to 20, provided that the sum of m and n is at least 3; and Y is selected from

wherein each occurrence of R³-R⁶is independently hydrogen or C₁-C₁₂hydrocarbyl; and a plurality of diisocyanate residue repeat units having the structure

wherein R⁷is, independently in each repeat unit, C₄-C₁₈hydrocarbyl; wherein at least one terminal oxygen atom of each poly(phenylene ether) repeat unit is covalently bonded to a terminal carbamoyl group of a diisocyanate residue repeat unit to form a urethane moiety.

Another embodiment is an article comprising the thermoplastic polyurethane.

Another embodiment is a method of forming a thermoplastic polyurethane, the method comprising: reacting a hydroxy-diterminated poly(phenylene ether) with an organic diisocyanate to form a thermoplastic polyurethane; wherein the hydroxy-diterminated poly(phenylene ether) has the structure

wherein each occurrence of R³-R⁶is independently hydrogen or C₁-C₁₂hydrocarbyl.

These and other embodiments are described in detail below.

BRIEF DESCRIPTION OF THE FIGURES

FIG. 1 is a plot of isocyanate concentration versus time for the reactions of Examples 1, 2, and 3.

FIG. 2 is a plot of isocyanate concentration versus time for the reactions of Examples 1 and 4.

FIG. 3 is a plot of reciprocal isocyanate concentration versus time for the reactions of Examples 1 and 4.

FIG. 4 is a plot of reciprocal isocyanate concentration versus time for the reaction of Example 2.

FIG. 5 is a plot of reciprocal isocyanate concentration versus time for the reaction of Example 3.

DETAILED DESCRIPTION OF THE INVENTION

The present inventor has prepared a thermoplastic polyurethane that incorporates specific poly(phenylene ether) segments and exhibits improvements in one or more of reduced moisture absorption, increased heat resistance, and increased strength at high elongation.

wherein R⁷is, independently in each repeat unit, C₄-C₁₈hydrocarbyl; wherein at least one terminal oxygen atom of each poly(phenylene ether) repeat unit is covalently bonded to a terminal carbamoyl group of a diisocyanate residue to form a urethane moiety.

As used herein, the term “plurality” means at least three. The term “hydrocarbyl”, whether used by itself, or as a prefix, suffix, or fragment of another term, refers to a residue that contains only carbon and hydrogen unless it is specifically identified as “substituted hydrocarbyl”. The hydrocarbyl residue can be aliphatic or aromatic, straight-chain, cyclic, bicyclic, branched, saturated, or unsaturated. It can also contain combinations of aliphatic, aromatic, straight chain, cyclic, bicyclic, branched, saturated, and unsaturated hydrocarbon moieties. When the hydrocarbyl residue is described as substituted, it can contain heteroatoms in addition to carbon and hydrogen. For example, Q¹can be a di-n-butylaminomethyl group formed by reaction of a terminal 3,5-dimethyl-1,4-phenyl group with the di-n-butylamine component of an oxidative polymerization catalyst,

In the poly(phenylene ether) repeat unit structure, each occurrence of Q¹is independently halogen, C₁-C₁₂hydrocarbyloxy, C₂-C₁₂halohydrocarbyloxy wherein at least two carbon atoms separate the halogen and oxygen atoms, or unsubstituted or substituted C₁-C₁₂hydrocarbyl provided that the hydrocarbyl group is not tertiary hydrocarbyl, C₁-C₁₂hydrocarbylthio; each occurrence of Q²is independently hydrogen, halogen, C₁-C₁₂hydrocarbylthio, C₁-C₁₂hydrocarbyloxy, C₂-C₁₂halohydrocarbyloxy wherein at least two carbon atoms separate the halogen and oxygen atoms, or unsubstituted or substituted C₁-C₁₂hydrocarbyl provided that the hydrocarbyl group is not tertiary hydrocarbyl. In some embodiments, each occurrence of Q¹is independently C₁-C₁₂alkyl, especially methyl. In some embodiments, each occurrence of Q²is independently hydrogen or methyl.

Also in the poly(phenylene ether) repeat unit structure, each occurrence of R¹and R²is independently hydrogen, halogen, C₁-C₁₂hydrocarbylthio, C₁-C₁₂hydrocarbyloxy, C₂-C₁₂halohydrocarbyloxy wherein at least two carbon atoms separate the halogen and oxygen atoms, or unsubstituted or substituted C₁-C₁₂hydrocarbyl provided that the hydrocarbyl group is not tertiary hydrocarbyl. In some embodiments, each occurrence of R¹is methyl, and each occurrence of R²is hydrogen. In general, m and n are independently 0 to 20, provided that the sum of m and n is at least 3. In some embodiments, the sum of m and n is 4 to 16. In general, Y is selected from

wherein each occurrence of R³-R⁶is independently hydrogen or C₁-C₁₂hydrocarbyl. In some embodiments Y is

wherein each occurrence of R³is independently hydrogen or C₁-C₆alkyl. In some embodiments, each occurrence of R³is methyl.

In some embodiments, the poly(phenylene ether) repeat unit has the structure

wherein each occurrence of Q⁵and Q⁶is independently methyl or di-n-butylaminomethyl; and each occurrence of a and b is independently 0 to 20, provided that the sum of a and b is at least 3. In some embodiments, the sum of a and b is 4 to 16.

In addition to the poly(phenylene ether) units, the thermoplastic polyurethane comprises a plurality of diisocyanate residue repeat units having the structure

wherein R⁷is, independently in each repeat unit, C₄-C₁₈hydrocarbyl. The diisocyanate residue repeat units are the residue of the organic diisocyanate reactant, many examples of which are described below. In some embodiments, each diisocyanate residue repeat unit independently has a structure selected from

At least one terminal oxygen atom of each poly(phenylene ether) repeat unit is covalently bonded to a terminal carbamoyl group of a diisocyanate residue repeat unit to form a urethane moiety (—O—C(═O)—NH—). An example of such a urethane linkage between a poly(phenylene ether) repeat unit and a diisocyanate residue repeat unit is illustrated by the structure below

In addition to the poly(phenylene ether) repeats units and the diisocyanate residue repeat units, the thermoplastic polyurethane can, optionally, further comprise a plurality of diol repeat units. The diol repeat units are distinct from the poly(phenylene ether) repeats units. Each diol repeat unit can be the residue of an alkylene diol, an alkylene ether diol, a polyether diol, an alkoxylate of an aromatic diol, or a polyester diol.

Examples of alkylene diols include 1,2-ethandiol (ethylene glycol), 1,2-propanediol (propylene glycol), 1,4-butanediol, 2-ethyl-1,3-hexanediol, 1,3-butanediol, 2-butyl-2-ethyl-1,3-propanediol, 2,4-diethyl-1,5-pentanediol, ethylene glycol, 1,3-propanediol, 2,3-butanediol, 1,5-pentanediol, 1,6-hexanediol, 2,2,4-trimethyl-1,3-pentanediol, and combinations thereof.

Examples of alkylene ether diols include diethylene glycol, triethylene glycol, tetraethylene glycol, dipropylene glycol, tripropylene glycol, tetrapropylene glycol, dibutylene glycol, tributylene glycol, tetrabutylene glycol, and combinations thereof.

Examples of polyether diols include polyethylene ether diols, polypropylene ether diols, polybutylene glycols, polytetramethylene ether diols, ethylene oxide capped polypropylene oxides, and combinations thereof.

Examples of alkoxylates of aromatic diols include ethoxylated and propoxylated derivatives of hydroquinone, resorcinol, catechol, 1,1-bis(3,5-dimethyl-4-hydroxyphenyl)ethane, 1,1-bis(3-chloro-4-hydroxyphenyl)ethane, 1,1-bis(3-methyl-4-hydroxyphenyl)-ethane, 1,2-bis(4-hydroxy-3,5-dimethylphenyl)-1,2-diphenylethane, 1,2-bis(3-methyl-4-hydroxyphenyl)-1,2-diphenylethane, 1,2-bis(3-methyl-4-hydroxyphenyl)ethane, 2,2′-binaphthol, 2,2′-biphenol, 2,2′-dihydroxy-4,4′-dimethoxybenzophenone, 2,2′-dihydroxy-4-methoxybenzophenone, 2,2′-dihydroxybenzophenone, 2,2-bis(3,5-dichloro-4-hydroxyphenyl)propane, 2,2-bis(3-bromo-4-hydroxyphenyl)propane, 2,2-bis(3-phenyl-4-hydroxyphenyl)propane, 2,2-bis(3-methyl-4-hydroxyphenyl)propane, 2,2-bis(3,5-dimethyl-4-hydroxyphenyl)propane, 1,1-bis(3,5-dimethyl-4-hydroxyphenyl)-1-phenylethane, 1,1-bis(3-chloro-4-hydroxyphenyl)-1-phenylethane, 1,1-bis(3-methyl-4-hydroxyphenyl)-1-phenylethane, 2,2-bis(4-hydroxy-3,5-dimethyl phenyl)-1-phenylpropane, 2,2-bis(4-hydroxy-3,5-dimethyl phenyl)hexane, 2,2-bis(4-hydroxy-3,5-dimethylphenyl)pentane, 2,2-bis(3-methyl-4-hydroxynaphthyl)propane, 2,2-bis(3-methyl-4-hydroxyphenyl)-1-phenylpropane, 2,2-bis(3-methyl-4-hydroxyphenyl)hexane, 2,2-bis(3-methyl-4-hydroxyphenyl)pentane, 2,2′-methylenebis(4-methylphenol), 2,2′-methylenebis[4-methyl-6-(1-methylcyclohexyl)phenol], 3,3′,5,5′-tetramethyl-4,4′-biphenol, 3,3′-dimethyl-4,4′-biphenol, bis(2-hydroxyphenyl)-methane, bis(4-hydroxy-2,6-dimethyl-3-methoxyphenyl)methane, bis(3,5-dimethyl-4-hydroxyphenyl)methane, bis(3-methyl-4-hydroxyphenyl)methane, bis-(4-hydroxy-3,5-dimethyl phenyl)cyclohexylmethane, bis(4-hydroxy-3,5-dimethyl phenyl)phenylmethane, bis(3-methyl-4-hydroxyphenyl)cyclohexylmethane, bis(3-methyl-4-hydroxyphenyl)methane, bis(3,5-dimethyl-4-hydroxyphenyl)methane, bis(3-methyl-4-hydroxyphenyl)phenylmethane, 2,2′,3,3′,5,5′-hexamethyl-4,4′-biphenol, octafluoro-4,4′-biphenol, 2,3,3′,5,5′-pentamethyl-4,4′-biphenol, 1,1-bis(3,5-dibromo-4-hydroxyphenyl)cyclohexane 1,1-bis(3,5-dimethyl-4-hydroxyphenyl)cyclohexane, bis(3-methyl-4-hydroxyphenyl)cyclohexane, tetrabromobiphenol, tetrabromobisphenol A, tetrabromobisphenol S, 2,2′-diallyl-4,4′-bisphenol A, 2,2′-diallyl-4,4′-bisphenol S, 3,3′,5,5′-tetramethyl-4,4′-bisphenol sulfide, 3,3′-dimethyl bisphenol sulfide, and 3,3′,5,5′-tetramethyl-4,4′-bisphenolsulfone.

Examples of polyester diols include aliphatic polyester diols (sometimes called aliphatic polyester polyols), aromatic polyester diols (sometimes called aromatic polyester polyols), and polycaprolactone diols. It will be understood that aromatic polyester diols include aromatic repeat units and can, optionally, further include aliphatic repeat units, as in poly(ethylene terephthalate) and poly(butylene terephthalate).

Since unreacted groups at the end of the polymer chain can undergo additional reactions during melt processing the thermoplastics polyurethane, a monohydric phenol or a monohydric alcohol or a monoisocyanate can be used to end-cap the polymer to control molecular weight and give more stable material.

The weight percent of poly(phenylene ether) repeat units and diisocyanate residue repeat units in the thermoplastic polyurethane will depend on the molecular weights of the hydroxy-diterminated poly(phenylene ether) and the organic diisocyanate from which the thermoplastic polyurethane is formed. In general, the thermoplastic polyurethane will comprise 5 to 95 weight percent of the poly(phenylene ether) repeat units, and 5 to 40 weight percent of the diisocyanate residue repeat units, based on the weight of the thermoplastic polyurethane. The thermoplastic polyurethane can, optionally, further comprise 5 to 70 weight percent of diol repeat units, each diol repeat unit comprising the residue of an alkylene diol, an alkylene ether diol, a polyether diol, an alkoxylate of an aromatic diol, or a polyester diol.

In some embodiments, the thermoplastic polyurethane has a weight average molecular weight of 10,000 to 250,000 atomic mass units, specifically 50,000 to 250,000 atomic mass units.

In a very specific embodiment of the thermoplastic polyurethane, the poly(phenylene ether) repeat units have the structure

wherein each occurrence of Q⁵and Q⁶is independently methyl or di-n-butylaminomethyl; and each occurrence of a and b is independently 0 to 20, provided that the sum of a and b is at least 3; the diisocyanate residue repeat units have a structure selected from

and the thermoplastic polyurethane further comprises a plurality of diol repeat units, each diol repeat unit comprising the residue of an alkylene diol, an alkylene ether diol, a polyether diol, an alkoxylate of an aromatic diol, or a polyester diol.

The invention includes articles formed from the thermoplastic polyurethane. Suitable methods of forming such articles include single layer and multilayer sheet extrusion, injection molding, blow molding, film extrusion, profile extrusion, pultrusion, compression molding, thermoforming, pressure forming, hydroforming, vacuum forming, and the like. Combinations of the foregoing article fabrication methods can be used. In some embodiments, the article is formed by injection molding or profile extrusion. Examples are articles that can be formed by extrusion include cable sheathing, spiral tubing, pneumatic tubing, blow molded bellows, and films Examples of articles that can be formed by injection molding include ski boot shells, sport shoe soles, caster tires, automotive body panels, and automotive rocker panels.

The invention includes a method of forming a thermoplastic polyurethane, the method comprising: reacting a hydroxy-diterminated poly(phenylene ether) with an organic diisocyanate to form a thermoplastic polyurethane; wherein the hydroxy-diterminated poly(phenylene ether) has the structure

wherein each occurrence of R³-R⁶is independently hydrogen or C₁-C₁₂hydrocarbyl; and wherein the organic diisocyanate has the structure
O═C═N—R⁷—N═C═O
wherein R⁷is C₄-C₁₈hydrocarbylene.

All of the structural variations described above for the poly(phenylene ether) repeat units apply as well to the hydroxy-diterminated poly(phenylene ether)s from which they are derived. Methods of preparing hydroxy-diterminated poly(phenylene ether)s are known. For example, they can be prepared by copolymerization of a monohydric phenol and a dihydric phenol as described, for example, in U.S. Pat. No. 7,541,421 to Carrillo et al. Hydroxy-diterminated poly(phenylene ether)s are also commercially available as, for example, PPO™ SA90 resin from Sabic Innovative Plastics.

Examples of organic diisocyanates that can be used in the reaction include 1,4-tetramethylene diisocyanate, 1,6-hexamethylene diisocyanate, 2,2,4-trimethyl-1,6-hexamethylene diisocyanate, 1,12-dodecamethylene diisocyanate, cyclohexane-1,3-diisocyanate, and cyclohexane-1,4-diisocyanate, 1-isocyanato-2-isocyanatomethyl cyclopentane, 1-isocyanato-3-isocyanatomethyl-3,5,5-trimethyl-cyclohexane (isophorone diisocyanate or IPDI), bis(4-isocyanatocyclohexyl)methane, 2,4′-dicyclohexyl-methane diisocyanate, 1,3-bis(isocyanatomethyl)-cyclohexane, 1,4-bis-(isocyanatomethyl)-cyclohexane, bis(4-isocyanato-3-methyl-cyclohexyl)methane, alpha,alpha,alpha′,alpha′-tetramethyl-1,3-xylylene diisocyanate, alpha,alpha,alpha′,alpha′-tetramethyl-1,4-xylylene diisocyanate, 1-isocyanato-1-methyl-4(3)-isocyanatomethyl cyclohexane, 2,4-hexahydrotoluene diisocyanate, 2,6-hexahydrotoluene diisocyanate, 1,3-phenylene diisocyanate, 1,4-phenylene diisocyanate, 2,4-toluene diisocyanate, 2,6-toluene diisocyanate, 2,4-diphenylmethane diisocyanate, 4,4′-diphenylmethane diisocyanate, 1,5-diisocyanato naphthalene, and mixtures thereof. In some embodiments, the diisocyanate comprises 1,6-hexamethylene diisocyanate, 1-isocyanato-3-isocyanatomethyl-3,5,5-trimethylcyclohexane (isophorone diisocyanate or IPDI), bis-(4-isocyanatocyclohexyl)methane, alpha,alpha,alph′,alpha′-tetramethyl-1,3-xylylene diisocyanate, alpha,alpha,alph′,alpha′-tetramethyl-1,4-xylylene diisocyanate, 1-isocyanato-1-methyl-4(3)-isocyanatomethyl cyclohexane, 2,4-hexahydrotoluene diisocyanate, 2,6-hexahydrotoluene diisocyanate, 2,4-toluene diisocyanate, 2,6-toluoylene diisocyanate, 2,4-diphenylmethane diisocyanate, 4,4′-diphenylmethane diisocyanate, 3,3-dimethyl-4,4-biphenyldiisocyanate, naphthalene-1,5-diisocyanate, 1-isocyanato-3-isocyanatomethyl-3,5,5-trimethylcylohexane, polyphenylene diisocyanate, or a mixture thereof.

As described above, the organic diisocyanate can be reacted with a diol in addition to the hydroxy-diterminated poly(phenylene ether). The diol is selected from alkylene diols, alkylene ether diols, polyether diols, alkoxylates of aromatic diols, polyester diols, and combinations thereof.

The organic diisocyanate can, optionally, be reacted with a diamine in addition to the hydroxy-diterminated poly(phenylene ether). Specific diamines include, for example, toluenediamines, dimethylthiotoulenediamines, 3,5-diethyltoluene-2,4-diamine, 3,5-diethyltoluene-2,6-diamine, methylenebis(2,6-diethylaniline), and combinations thereof. When a diamine is employed, the product polyurethane comprises repeating units in which each amine group has reacted with an isocyanate group to form a urea moiety.

Reacting the organic diisocyanate with the hydroxy-diterminated poly(phenylene ether) and, optionally, the diol, yields a linear thermoplastic polyurethane. If a branched or crosslinked polyurethane is desired, a poly(phenylene ether) having more than two hydroxy groups and/or an isocyanate compound having more than two isocyanate groups and/or a polyol having at least three hydroxyl groups can be employed.

As illustrated in the working examples below, reacting the hydroxy-diterminated poly(phenylene ether) with the organic diisocyanate can be conducted in the absence of a catalyst.

Alternatively, and also as illustrated in the working examples below, the reaction can be conducted in the presence of a catalyst. Suitable catalysts include tertiary amines and metal compounds based on tin, bismuth, and zinc. Tertiary amine catalysts include triethylenediamine (TEDA, 1,4-diazabicyclo[2.2.2]octane or DABCO), dimethylcyclohexylamine (DMCHA), dimethylethanolamine (DMEA), and N-ethylmorpholine. Specific metal compounds include bismuth and zinc carboxylates, organotin compounds (including dibutyltin dilaurate and tin carboxylates such as stannous octoate), oxides of tin, bismuth and zinc, and mercaptides of tin, bismuth, and zinc.

Reacting the hydroxy-diterminated poly(phenylene ether) with the organic diisocyanate can be conducted in the presence of a solvent. Suitable solvents include aromatic solvents, such as toluene, ethylbenzene, xylenes, anisole, chlorobenzene, dichlorobenzenes, and combinations thereof.

Alternatively, reacting the hydroxy-diterminated poly(phenylene ether) with the organic diisocyanate can be conducted in the absence of a solvent, that is, in bulk.

In a very specific embodiment of the method of forming a thermoplastic polyurethane, the hydroxy-diterminated poly(phenylene ether) has the structure

wherein each occurrence of Q⁵and Q⁶is independently methyl or di-n-butylaminomethyl, and each occurrence of a and b is independently 0 to 20, provided that the sum of a and b is at least 3; the organic diisocyanate is selected from the group consisting of 2,4′-diphenylmethane diisocyanate, 4,4′-diphenylmethane diisocyanate, toluene 2,6-diisocyanate, toluene 2,4-diisocyanate, and combinations thereof; and the method comprises reacting the organic diisocyanate with the hydroxy-diterminated poly(phenylene ether) and a diol selected from the group consisting of alkylene diols, alkylene ether diols, polyether diols, alkoxylates of aromatic diols, polyester diols, and combinations thereof.

All ranges disclosed herein are inclusive of the endpoints, and the endpoints are independently combinable with each other.

The invention includes at least the following embodiments.

Embodiment 1

A thermoplastic polyurethane comprising: a plurality of poly(phenylene ether) repeat units having the structure

Embodiment 2

The thermoplastic polyurethane of embodiment 1, wherein the poly(phenylene ether) repeat units have the structure

wherein each occurrence of Q⁵and Q⁶is independently methyl or di-n-butylaminomethyl; and each occurrence of a and b is independently 0 to 20, provided that the sum of a and b is at least 3.

Embodiment 3

The thermoplastic polyurethane of

embodiment

1 or 2, wherein each diisocyanate residue repeat units independently has a structure selected from

Embodiment 4

The thermoplastic polyurethane of any of embodiments 1-3, further comprising a plurality of diol repeat units, each diol repeat unit comprising the residue of an alkylene diol, an alkylene ether diol, a polyether diol, an alkoxylate of an aromatic diol, or a polyester diol.

Embodiment 5

The thermoplastic polyurethane of any of embodiments 1-3, comprising 5 to 95 weight percent of the poly(phenylene ether) repeat units, and 5 to 40 weight percent of the diisocyanate residue repeat units.

Embodiment 6

The thermoplastic polyurethane of embodiment 5, further comprising 5 to 70 weight percent of diol repeat units, each diol repeat unit comprising the residue of an alkylene diol, an alkylene ether diol, a polyether diol, an alkoxylate of an aromatic diol, or a polyester diol.

Embodiment 7

The thermoplastic polyurethane of any of embodiments 1-6, having a weight average molecular weight of 10,000 to 250,000 atomic mass units.

Embodiment 8

wherein each occurrence of Q⁵and Q⁶is independently methyl or di-n-butylaminomethyl; and each occurrence of a and b is independently 0 to 20, provided that the sum of a and b is at least 3; wherein the diisocyanate residue repeat units have a structure selected from

and wherein the thermoplastic polyurethane further comprises a plurality of diol repeat units, each diol repeat unit comprising the residue of an alkylene diol, an alkylene ether diol, a polyether diol, an alkoxylate of an aromatic diol, or a polyester diol.

Embodiment 9

An article comprising a thermoplastic polyurethane comprising: a plurality of poly(phenylene ether) repeat units having the structure

wherein each occurrence of Q¹is independently halogen, unsubstituted or substituted C₁-C₁₂hydrocarbyl provided that the hydrocarbyl group is not tertiary hydrocarbyl, C₁-C₁₂hydrocarbylthio, C₁-C₁₂hydrocarbyloxy, or C₂-C₁₂halohydrocarbyloxy wherein at least two carbon atoms separate the halogen and oxygen atoms; each occurrence of Q²is independently hydrogen, halogen, unsubstituted or substituted C₁-C₁₂hydrocarbyl provided that the hydrocarbyl group is not tertiary hydrocarbyl, C₁-C₁₂hydrocarbylthio, C₁-C₁₂hydrocarbyloxy, or C₂-C₁₂halohydrocarbyloxy wherein at least two carbon atoms separate the halogen and oxygen atoms; each occurrence of R¹and R²is independently hydrogen, halogen, unsubstituted or substituted C₁-C₁₂hydrocarbyl provided that the hydrocarbyl group is not tertiary hydrocarbyl, C₁-C₁₂hydrocarbylthio, C₁-C₁₂hydrocarbyloxy, or C₂-C₁₂halohydrocarbyloxy wherein at least two carbon atoms separate the halogen and oxygen atoms; m and n are independently 0 to 20, provided that the sum of m and n is at least 3; and Y is selected from

Embodiment 10

The article of embodiment 9, wherein the article is selected from the group consisting of films, cable sheathing, spiral tubing, pneumatic tubing, blow molded bellows, ski boot shells, sport shoe soles, caster tires, automotive body panels, and automotive rocker panels.

Embodiment 11

A method of forming a thermoplastic polyurethane, the method comprising: reacting a hydroxy-diterminated poly(phenylene ether) with an organic diisocyanate to form a thermoplastic polyurethane; wherein the hydroxy-diterminated poly(phenylene ether) has the structure

Embodiment 12

The method of embodiment 11, comprising reacting the organic diisocyanate with the hydroxy-diterminated poly(phenylene ether) and a diol selected from the group consisting of alkylene diols, alkylene ether diols, polyether diols, alkoxylates of aromatic diols, polyester diols, and combinations thereof.

Embodiment 13

The method of embodiment 11 or 12, wherein said reacting is conducted in the absence of a catalyst.

Embodiment 14

The method of embodiment 11 or 12, wherein said reacting is conducted in the presence of a catalyst.

Embodiment 15

The method of any of embodiments 11-14, wherein said reacting is conducted in the absence of solvent.

Embodiment 16

The method of embodiment 11, wherein the hydroxy-diterminated poly(phenylene ether) has the structure

wherein each occurrence of Q⁵and Q⁶is independently methyl or di-n-butylaminomethyl, and each occurrence of a and b is independently 0 to 20, provided that the sum of a and b is at least 3; wherein the organic diisocyanate is selected from the group consisting of 2,4′-diphenylmethane diisocyanate, 4,4′-diphenylmethane diisocyanate, toluene 2,6-diisocyanate, toluene 2,4-diisocyanate, and combinations thereof and wherein the method comprises reacting the organic diisocyanate with the hydroxy-diterminated poly(phenylene ether) and a diol selected from the group consisting of alkylene diols, alkylene ether diols, polyether diols, alkoxylates of aromatic diols, polyester diols, and combinations thereof.

The invention is further illustrated by the following non-limiting examples.

Materials and Methods

Reagents used in the synthesis of thermoplastic polyurethanes are summarized in Table 1.

TABLE 1

Reagent	Description

PPE-OH₂0.06	Copolymer of 2,6-dimethylphenol and 2,2-bis(3,5-dimethyl-4-
	hydroxyphenyl)propane, CAS Reg. No. 1012321-47-9, having an intrinsic
	viscosity of 0.06 deciliter per gram, a hydroxyl-equivalent weight of 681
	grams/mole; titration of hydroxyl groups required 82.4 milligrams
	potassium hydroxide per gram of oligomer; preparable according to the
	procedure of Example 4 of U.S. Pat. No. 7,541,421.
PPE-OH₂0.09	Copolymer of 2,6-dimethylphenol and 2,2-bis(3,5-dimethyl-4-
	hydroxyphenyl)propane, CAS Reg. No. 1012321-47-9, having an intrinsic
	viscosity of 0.09 deciliter per gram, a hydroxyl-equivalent weight of 924
	grams/mole; titration of hydroxyl groups required 60.7 milligrams
	potassium hydroxide per gram of oligomer; available as PPO ™ SA90 resin
	from Sabic Innovative Plastics.
PPE-OH₂0.12	Copolymer of 2,6-dimethylphenol and 2,2-bis(3,5-dimethyl-4-
	hydroxyphenyl)propane, CAS Reg. No. 1012321-47-9, having an intrinsic
	viscosity of 0.12 deciliter per gram, a hydroxyl-equivalent weight of 1597
	grams/mole; titration of hydroxyl groups required 35.1 milligrams
	potassium hydroxide per gram of oligomer; preparable according to the
	procedure of Example 1 of U.S. Pat. No. 7,541,421.
Polyether diol 1	Poly(oxytetramethylene) glycol, CAS Reg. No. 25190-06-1, having a
	hydroxyl equivalent weight of 524.8; titration of hydroxyl groups required
	106.9 milligrams potassium hydroxide per gram glycol; available as
	TERATHANE ™ 1000 from Invista.
Polyether diol 2	Ethylene oxide-capped oxypropylated polyether diol; titration of hydroxyl
	groups required 56.7 milligrams potassium hydroxide per gram diol;
	available as Poly-G-55-56 from Arch Chemicals.
Polyester diol 1	Poly(butylene adipate) polyester diol, CAS Reg. No. 25103-87-1, having a
	hydroxyl equivalent weight of 1,003; titration of hydroxyl groups required
	55.9 milligrams potassium hydroxide per gram diol; available as Poly S
	2000BA from itwc inc.
Polyester diol 2	Ortho phthalate-diethylene glycol-based aromatic polyester polyol, CAS
	Reg. No. 32472-85-8, having a hydroxyl equivalent weight of 323.6;
	titration of hydroxyl groups required 173.37 milligrams potassium
	hydroxide per gram diol; available as STEPANPOL ™ PS 1752 from
	Stepan.
2,4′-/4,4′-MDI	A mixture of 2,4′-diphenylmethane diisocyanate, CAS Reg. No.
	5873-54-1, and 4,4′-diphenylmethane diisocyanate, CAS Reg. No. 101-68-
	8, having an isocyanate (NCO) content of 33.4%; available as
	MONDUR ™ MLQ from Bayer.
4,4′- MDI	4,4′-diphenylmethane diisocyanate, CAS Reg. No. 101-68-8, having an
	isocyanate (NCO) content of 33.6%; available as MONDUR ™ M from
	Bayer.
TDI	A mixture of toluene 2,6-diisocyanate, CAS Reg. No. 91-08-7, and toluene
	2,4-diisocyanate, CAS Reg. No. 584-84-9, having an isocyanate (NCO)
	content of 47.98%; available as LUPRANATE ™ T80 from BASF.
HQEE	Hydroquinone bis(2-hydroxyethyl) ether, CAS Reg. No. 104-38-1, having
	a hydroxyl equivalent weight of 99.1; available Sigma-Aldrich.
BD	1,4-Butanediol, CAS Reg. No. 110-63-4, having a hydroxyl equivalent
	weight of 45; available from Alfa Aesar.
Amine curative	A mixture of aromatic diamines consisting primarily of 3,5-diethyltoluene-
	2,4-diamine, CAS Reg. No. 2095-02-5, and 3,5-diethyltoluene-2,6-
	diamine, CAS Reg. No. 2095-01-4; having an amine equivalent weight of
	81.9; available as ETHACURE ™ 100 from Albemarle Corp.
Dibutyltin	Dibutyltin dilaurate (catalyst), CAS Reg. No. 77-58-7; available as
dilaurate	DABCO ™ T-12 from Air Products.

The following test methods were used to characterize the thermoplastic polyurethanes.

Physico-mechanical properties. Shore A and Shore D hardness values, which are unitless, were determined at 23° C. according to ASTM D 2240-05 (2010). Tensile strength values, expressed in units of megapascals, and tensile elongation values, expressed in units of percent, were determined at 23° C. according to ASTM D 412-06a(2013), Test Method A, using an Instron Universal Tester, Model 1122 and a test speed of 50.8 centimeters/minute (20 inches/minute). Tear strength values, expressed in units of Newtons/centimeter, were determined at 23° C. according to ASTM D 624-00 (2012), using an Instron Universal Tester, Model 1122, Die C, and a test speed of 50.8 centimeters/minute (20 inches/minute). Compression set values, expressed in units of percent, were determined at 23° C. according to ASTM D 395-03 (2008). Bayshore resilience values, expressed in units of percent, were determined at 23° C. according to ASTM D 2632-01 (2008). Taber abrader test weight loss values, expressed in units of percent, was determined using a Taber Abrader, 2000 cycles, CALIBRADE™ H-22 abrasion wheels, and a 500 gram weight.

Morphology and thermal properties. Glass transition temperature (T_g) values, expressed in units of degrees centigrade, were determined according to ASTM D 3418-12e1 using a TA Instruments DSC Q10 and a thermal cycle with equilibration at −80° C. followed by heating at 20° C./minute to 200° C. Glass transition temperature was also determined by Dynamic Mechanical Analysis (DMA) using a TA Instruments DMA 2980, a nitrogen atmosphere, a temperature range of −80 to 130° C., a heating rate of 3° C./minute, and a frequency of 10 hertz. Coefficient of Thermal Expansion (CTE) values, expressed in units of micrometer/meter-° C., were determined by Thermomechanical Analysis (TMA) using a TA Instruments TMA Q400, a nitrogen atmosphere, a temperature range of −80 to 130° C., and a heating rate of 10° C./minute. Heat resistance was estimated by measuring tensile properties at 50 and 70° C. Thermal and oxidative stability were estimated by determining the change in tensile stress-strain properties and glass transition temperature after exposure to 100° C. for seven days in an air atmosphere. Dielectric Constant and Dissipation Factor, both unitless, were determined using parallel plates on a 76A 1 Megahertz Automatic Capacitance Bridge (Boonton Electronics, Model 76A).

Solvent resistance and hydrolytic stability. Acid resistance was determined by immersing a sample for three days immersion in pH 1 hydrochloric acid at 23° C. and expressed as a post-test sample weight (%) relative to pre-test sample weight of 100%. Base resistance was determined by immersing a sample for three days in pH 13 sodium hydroxide at 23° C. and expressed as a post-test sample weight (%) relative to pre-test sample weight of 100%. Solvent resistance was determined by immersing a sample for three days in toluene, methyl ethyl ketone (MEK), or Mobil Vacuum Pump Oil (SAE Grade 20, ISO Viscosity Grade 68) at 23° C. and expressed as a post-test sample weight (%) relative to pre-test sample weight of 100%. Water absorption was determined by the percent weight change after seven days exposure to 50° C., 100% relative humidity air.

Weight average molecular weight (M_w) and number average molecular weight (M_n), each expressed in atomic mass units (amu), were determined using an Agilent 1100 Series HPLC System with two Phenomenex PHENOGEL™ 5 micrometer Linear columns and a UV detector. Chloroform with 50 parts per million dibutyl amine was the eluent. The injection volume was 50 microliters. Molecular weight values were uncorrected from polystyrene standards.

Weight percent char was determined using a TGA Perkin Elmer Pyris 1. The samples were heat from 50 to 800° C. at 20 degrees per minute in air and nitrogen. The residue at 600, 700, and 800° C. was the percent char.

Kinetics of polyurethane formation. Kinetic data on the reaction of PPE-OH₂0.09 with 4,4′-MDI were determined at 50° C., 60° C., and 70° C. The kinetic measurement for the reaction of PPE-OH₂0.09 with 4,4′-MDI was carried out in a three necked 300 milliliter cylindrical flask equipped with a magnetic stirrer, reflux condenser, thermocouple, and nitrogen inlet. The reaction flask was heated via a heating mantle equipped with a temperature controller. The reaction temperature was maintained during reactions at ±1° C.

PPE-OH₂0.09 (0.039 equivalents) was pre-dissolved in 95 milliliters of dry toluene at room temperature with stirring on a stirrer plate. The PPE-OH₂0.09 was added incrementally in small portions to toluene over one hour. The resulting homogeneous toluene solution of PPE-OH₂0.09 was transferred into a volumetric cylinder and adjusted to a total volume of 100 milliliters by adding dry toluene. This solution was transferred into a reaction flask and heated while mixing to a desired temperature under continuous flow of nitrogen. 4,4′-MDI (0.045 equivalents), which was previously preheated at 80° C., was weighed into a 25 milliliter volumetric flask and toluene was added up to 25 milliliter mark, mixed thoroughly to homogenize and heated to temperature of the reaction. Once the temperature in the reaction flask reached a desired temperature, the solution of diisocyanate was added via funnel to the solution of PPE-OH₂0.09. The time when approximately half of the solution was added to the flask was taken as the starting time of reaction. At certain time intervals, samples of the reaction solution were removed and isocyanate content determined via di-n-butyl amine titration (according to the ASTM D 5155-10 test method).

Example 1

Kinetic data for the reaction of PPE-OH₂0.09 with 4,4′-MDI in toluene at 50° C. are presented in Table 2.

TABLE 2

Time (min)	NCO (%)	Diisocyanate (mol/kg)

0	1.27	0.151
30	1.15	0.137
60	1.06	0.126
120	0.87	0.104
150	0.89	0.106
180	0.8	0.095
210	0.78	0.093
240	0.71	0.085
300	0.63	0.075
350	0.57	0.068

Example 2

Kinetic data for the reaction of PPE-OH₂0.09 with 4,4′-MDI in toluene at 60° C. are presented in Table 3.

TABLE 3

Time (min)	NCO (%)	Diisocyanate (mol/kg)

0	1.27	0.151
20	1.16	0.138
60	1.05	0.125
80	0.96	0.114
100	1.00	0.119
120	0.87	0.104
140	0.87	0.104
160	0.84	0.100
180	0.74	0.088
200	0.67	0.080
220	0.68	0.081
240	0.63	0.075
260	0.54	0.064
300	0.58	0.069
320	0.49	0.058

Example 3

Kinetic data for the reaction of PPE-OH₂0.09 with 4,4′-MDI in toluene at 70° C. are presented in Table 4.

TABLE 4

Time (min)	NCO (%)	Diisocyanate (mol/kg)

0	1.27	0.151
25	1.23	0.146
40	1.05	0.125
60	0.99	0.118
80	1.11	0.132
100	0.93	0.111
120	0.79	0.094
140	0.69	0.082
180	0.58	0.069
220	0.45	0.054
240	0.43	0.051
260	0.4	0.048

Examples 1, 2, and 3 show the reaction of hydroxy-diterminated poly(phenylene ether) with diisocyanates without any catalyst. The reaction rate increases with increasing temperature. The data are compared in FIG. 1.

Example 4

This example illustrates the effect of 0.01% dibutyltin dilaurate catalyst on the reaction rate of PPE-OH₂0.09 with 4,4′-MDI in toluene at 50° C. Data are presented in Table 5.

TABLE 5

Time (min)	NCO (%)	Diisocyanate (mol/kg)

0	1.27	0.151
20	0.71	0.085
40	0.53	0.063
60	0.33	0.039
80	0.33	0.039
100	0.28	0.033
120	0.24	0.029
140	0.2	0.024
160	0.17	0.02

A comparison of Example 1 with Example 4 shows that the rate of reaction of PPE-OH₂0.09 with diisocyanate increased sharply (almost 12 times) in the presence of tin catalyst as measured in the reaction at 50° C. The data are compared in FIG. 2.

The reactions at 50° C. (with and without catalyst), at 60° C. and 70° C. followed second order reaction rates up to high degree of isocyanate conversion as shown in FIGS. 3, 4, and 5, respectively.

The kinetic parameters are summarized in Table 6, where “k” is the 2nd order reaction rate constant.

TABLE 6

	Catalyst	k × 100
Temp.	dibutyltin	(kg mol⁻¹	Half-time of	Correlation
(° C.)	dilaurate	min⁻¹)	reaction (min.)	coefficient, R²

Ex. 1	50	None	2.26	303	0.9834
Ex. 4	50	0.01%	25.42	26	0.9739
Ex. 2	60	None	3.23	208	0.9411
Ex. 3	70	None	6.23	107	0.9587

Examples 5-11 Preparative Examples

The solution polymerizations of PPE-OH₂0.09, other polyols co-monomers, and chain extenders with 2,4′-/4,4′-MDI were carried out in a three necked 500 milliliter cylindrical flask equipped with a mechanical stirrer, reflux condenser, thermocouple, and nitrogen inlet. The reaction flask was heated via a heating mantle equipped with a temperature controller. The reaction temperature was maintained during reactions at ±3° C.

The specified amount of dry toluene was added to reaction flask at room temperature. PPE-OH₂0.09 was added incrementally over one hour in small portions to toluene at 60° C. A co-polyol, chain extender, and catalyst were added directly to reaction flask and homogenized while stirring. The mixture was heated to the desired reaction temperature under continuous flow of nitrogen. A weighed amount of isocyanate was added via syringe to the reaction flask and this time was taken as the starting time of reaction. At certain time intervals, a sample of the reaction solution was taken and unreacted isocyanate content determined via di-n-butyl amine titration (ASTM D 5155-10). If the viscosity of polymer solution appeared to increase significantly during polymerization, additional toluene was added to the reaction mixture. Tables 7 and 8 specify the total amount of the toluene used in each synthesis.

The formulations for synthesis of thermoplastic polyurethanes using PPE-OH₂0.09, low molecular weight co-polyols, and chain extenders with 2,4′-/4,4′-MDI appear in Table 7. The formulations for synthesis of thermoplastic polyurethanes using PPE-OH₂0.09, high molecular weight co-polyols and chain extenders with 2,4′-/4,4′-MDI appear in Table 8.

TABLE 7

	Ex 5	Ex 6	Ex 7	Ex 8

REACTION COMPONENTS

PPE-OH₂0.09 (grams)	46.2	46.2	46.2	92.4
2,4′-/4,4′-MDI (grams)	6.3	12.7	12.8	—
Toluene diisocyanate	—	—	—	17.84
(grams)
1,4-Butanediol (grams)	—	2.25	—	—
Hydroquinone	—	—	4.96	—
bis(2-hydroxyethyl)
ether (grams)
Amine curative (grams)				1.102
Dibutyltin dilaurate (grams)	0.0278	0.0278	0.0278	0.04
Toluene (grams)	106.7	106.7	146	204.77
Solid content (%)	23.9	36.4	30.5	35.3
NCO/OH equivalent ratio	1.02	1.02	1.02	2.05

REACTION CONDITIONS

Temperature (° C.)	60	70	100	70
Time (min)	300	180	360	180

TABLE 8

Ex 9	Ex 10	Ex 11

REACTION COMPONENTS

PPE-OH₂0.09 (grams)	50	50	50
Poly(oxytetramethylene) glycol (grams)	50	—	—
Poly(butylene adipate) polyester diol	—	50	—
(grams)
Ortho phthalate-diethylene glycol based	—	—	50
aromatic polyester polyol (grams)
2,4′-/4,4′-MDI, (grams)	19.1	13.3	26.8
Dibutyltin dilaurate (grams)	0.04	0.04	0.0278
Toluene (grams)	193.4	202.2	193.4
Solid content (%)	38.1	34.1	39.6
NCO/OH equivalent ratio	1.02	1.02	1.02

REACTION CONDITIONS

Temperature (° C.)	70	80	80
Time (min)	300	360	300

The extent of the polymerization reaction of PPE-OH₂0.09, low molecular weight co-polyols, and chain extenders with 2,4′-/4,4′-MDI was followed by measuring the isocyanate levels (NCO %) at different time intervals during the syntheses via solution polymerization. Data for Examples 5, 6, 7, and 8 are shown in Table 9.

TABLE 9

Ex 5	Ex 6	Ex 7	Ex 8

Time (min)	NCO (%)

0	1.4	2.5	1.3	1.4
60	—	—	0.86	1.2
120	—	0.22	—	—
180	0.23	0.12	0.1	1.1
240	—	—	—	—
300	0.12	—	—	—
360	—	—	0.06	—

The extent of the polymerization reaction of PPE-OH₂0.09 and high molecular weight co-polyols with 2,4′-/4,4′-MDI was followed by measuring the isocyanate levels (NCO %) at different time intervals during the syntheses via solution polymerization. Data for Examples 9, 10, and 11 are shown in Table 10.

TABLE 10

Ex. 9	Ex. 10	Ex. 11

Time (min)	NCO (%)

0	2	1.5	2.8
60	0.32	0.3	—
120	0.29	0.28	0.43
180	—	0.26	0.31
240	0.18	—	—
300	0.12	0.16	0.2
360	—	0.13	—

The data in Tables 9 and 10 indicate that the hydroxy-diterminated poly(phenylene ether) along with the polyols react with the diisocyanates to give thermoplastic polyurethanes.

Films were cast from thermoplastic polyurethane solutions prepared in Examples 5-11 and were characterized. Data appear in Tables 11 and 12. All thermoplastic polyurethanes exhibited high glass transition temperatures (T_gvalues) and high char yields.

TABLE 11

Ex. 5	Ex. 6	Ex. 7	Ex. 8

Tg (° C.)	170.2	165.3	160.1	169
M_w(amu)	105,860	93,294	112,940	18,750
M_n(amu)	13,804	13,499	12,710	3,807
Char in nitrogen at	23.32	17.63	17.23	18.03
600° C. (wt %)
Char in nitrogen	21.05	16.07	15.77	16.48
at 700° C. (wt %)
Char in nitrogen	19.67	15.27	14.92	15.65
at 800° C. (wt %)
Char in air at	35.29	28.26	26.34	27.11
600° C. (wt %)
Char in air at	7.85	8.79	4.63	11.24
700° C. (wt %)
Char in air at	3.19	0.35	1.91	0.64
800° C. (wt %)

TABLE 12

Ex. 9	Ex. 10	Ex. 11

Tg (° C.)	ND	163.7	133.2
M_w(amu)	107330	62170	ND
M_n(amu)	14844	10094	ND
Tensile Strength @ Break (MPa)	19.42	24.52	ND
Tensile Strength @ Yield (MPa)	15.99	20.44	ND
Char in nitrogen at 600° C. (wt %)	10.53	11.16	ND
Char in nitrogen at 700° C. (wt %)	9.79	10.28	ND
Char in nitrogen at 800° C. (wt %)	9.33	9.8	ND
Char in air at 600° C. (wt %)	20.3	18.04	ND
Char in air at 700° C. (wt %)	5.97	4.6	ND
Char in air at 800° C. (wt %)	0.64	0.34	ND

ND = not determined

Examples 12 and 13

In Example 12, a polyurethane was synthesized from higher molecular weight hydroxy-diterminated poly(phenylene ether) (PPE-OH₂0.12) with 4,4′-MDI using the solution polymerization procedure.

In Example 13, a polyurethane was synthesized from lower molecular weight hydroxy-diterminated poly(phenylene ether) (PPE-OH₂0.06) with 4,4′-MDI using the solution polymerization procedure.

Formulation and characterization of Examples 12 and 13 are summarized in Table 13, where amounts of hydroxy-diterminated poly(phenylene ether) are expressed in weight percent based on the total weight of diol and diisocyanate, and amounts of dibutyltin dilaurate are expressed in parts per hundred weight resin (i.e., parts by weight per 100 parts by weight diol and diisocyanate). The thermoplastic polyurethanes formed in Examples 12 and 13 exhibited high T_gvalues and high char yield.

	TABLE 13

	Ex. 12	Ex. 13

REACTION COMPONENTS

PPE-OH₂0.12 (wt %)	92.48	—
PPE-OH₂0.06 (wt %)	—	83.98
2,4′-/4,4′-MDI, wt %	7.52	16.02
Dibutyltin dilaurate (phr)	0.0520	0.0540

PROPERTIES

Tg (° C.)	185	152
M_w(amu)	79,243	99,765
M_n(amu)	15764	12706
Char in nitrogen at 600° C. (wt %)	25.37	20.93
Char in nitrogen at 700° C. (wt %)	23.23	18.92
Char in nitrogen at 800° C. (wt %)	21.47	17.6
Char in air at 600° C. (wt %)	38.71	31.05
Char in air at 700° C. (wt %)	11.55	6.43
Char in air at 800° C. (wt %)	4.97	2.93

Example 14, Comparative Example A

Thermoplastic polyurethanes were prepared using bulk polymerization. The general procedure for bulk polymerization of hydroxy-diterminated poly(phenylene ether) and diols with diisocyanates to from TPUs was as follows:

- 1. A degassed, preheated mixture of hydroxy-diterminated poly(phenylene ether) and diols were added to a Speed Mixer cup;
- 2. The contents of the Speed Mixer cup were mixed for 30 seconds at 2200 rotations per minute (rpm);
- 3. The resulting mixture was heated for 15 minutes in an oven at 120° C.;
- 4. Liquid diisocyanate at 80° C. was added to the heated mixture via syringe;
- 5. The resulting mixture was mixed via Speed Mixer for 30 seconds at 2200 rpm;
- 6. The mixture was then transferred into a 120° C. aluminum mold covered with a sheet of polytetrafluoroethylene;
- 7. At the gel time, the mold was closed and the reaction advanced for 2 hours at 120° C.;
- 8. The reaction mixture was then further reacted for 20 hours at 100° C.;
- 9. Sheets of the resulting material were prepared by compression molding in a Carver press.

For Example 14, thermoplastic polyurethane was prepared by bulk polymerization using PPE-OH₂0.09, poly(oxytetramethylene) glycol, butanediol, and 4,4′-MDI. Formulation and characterization are summarized in Table 14. The material exhibits very high elongation at break which is characteristic of thermoplastic elastomers. Compared to Comparative Example A prepared without a hydroxy-diterminated poly(phenylene ether), Example 14 had higher VICAT softening temperature and higher char yield and better mechanical properties at elevated temperatures.

	TABLE 14

	C. Ex. A	Ex. 14

REACTION COMPONENTS

PTMG1000 (pbw)	63.82	49.67
PPE-OH₂0.09 (pbw)	0.00	16.56
4,4′-MDI (pbw)	30.70	28.74
BD (pbw)	5.48	5.03

PROPERTIES

Hardness Shore A	86	88
Hardness Shore D	37	40
Tensile Strength at break, 23° C. (MPa)	24.50	28.42
Elongation at break, 23° C. (%)	808	554
Max. Tear Strength - Die C (N/cm)	1305	833
Constant Deflection Compression Set, Ct (%)	6.1	6.6
Tensile Strength at break, 50° C. (MPa)	9.3	14.7
Elongation at break, 50° C. (%)	496	517
Tensile Strength at break, 70° C. (MPa)	6.7	9.2
Elongation at break, 70° C. (%)	502	443
VICAT A (° C.)	74.2	107.8
Char in nitrogen at 600° C. (wt %)	1.8	5.3
Char in nitrogen at 700° C. (wt %)	1.7	5.1
Char in nitrogen at 800° C. (wt %)	1.6	4.9
Char in air at 600° C. (wt %)	4.4	9.8
Char in air at 700° C. (wt %)	0.1	0.2
Char in air at 800° C. (wt %)	0.1	0.2
Oxidative Resistance at 100° C. for 7 days
Tensile Strength at break at 23° C. (MPa)	8.28	20.81
Elongation at break at 23° C. (%)	874	870
T_g(° C.)	−31	−27
Solvent resistance, post-test sample weight (%)
relative to pre-test sample weight of 100%
Toluene	81.2	53.1
MEK	Dissolved	117
Oil	0.33	0.06
Hydrochloric Acid, pH 1	1.5	1.2
Sodium hydroxide, pH 13	1.5	1.2
Hydrolytic Stability at 50° C. for 7 days,
Weight change (%)	1.5	1.2

Examples 15-17, Comparative Example B

A series of thermoplastic polyurethanes were prepared by bulk polymerization using hydroxy-diterminated poly(phenylene ether), Polyether diol 2 (Ethylene oxide-capped oxypropylated polyether diol), butanediol, and 4,4′-MDI. The hydroxy-diterminated poly(phenylene ether) content was 0, 10, 20, and 30 weight percent in Comparative Example B, Example 15, Example 16, and Example 17, respectively. Formulation and characterization are summarized in Table 15. All materials exhibited very high elongation at break, which is characteristic of thermoplastic elastomers. Char yield increased with hydroxy-diterminated poly(phenylene ether) levels. In addition, Taber abrasion decreased with increased levels of hydroxy-diterminated poly(phenylene ether). Moreover, tear strength increased with increased levels of hydroxy-diterminated poly(phenylene ether). Formulations and properties are summarized in Table 15.

TABLE 15

Formulation	C. Ex. B	Ex. 15	Ex. 16	Ex. 17

REACTION COMPONENTS

Polyether diol 2 (wt %)	76.70	68.89	61.17	53.67
PPE-OH₂0.09 (pbw)	—	7.65	15.29	23.00
4,4′-MDI (wt %)	19.99	19.95	20.02	20.34
BD (wt %)	3.31	3.51	3.52	2.99
Dibutyltin dilaurate (phr)	0.2160	0.0038	0.0267	0.0524

PROPERTIES

Hardness Shore A	43	62	63	83
Bayshore resilience (%)	58	42	25	16
Tensile Strength at break, 23° C. (MPa)	4.64	0.65	1.95	28.45
Elongation at break, 23° C. (%)	774	984	1115	549
Tensile Strength at yield, 23° C. (MPa)	—	0.69	5.43	—
Elongation at yield, 23° C. (%)	—	100	787	—
Tensile Strength at break, 50° C. (MPa)	2.24	0.26	0.62	7.46
Elongation at break, 50° C. (%)	504	487	478	359
Tensile Strength at break, 70° C. (MPa)	1.49	0.08	0.11	4.31
Elongation at break, 70° C. (%)		263	334	307
Max. Tear Strength - Die C (N/cm)	185	229	367	833
Constant Deflection Compression Set, Ct (%)	16	20.3	18	11
Taber Abrader Test Weight Loss (%)	0.0131	0.0109	0.0108	0.003
Char in nitrogen at 600° C. (wt %)	1.5	2.9	5	7
Char in nitrogen at 700° C. (wt %)	1.4	2.7	4.6	6.4
Char in nitrogen at 800° C. (wt %)	1.3	2.6	4.5	6
Char in air at 600° C. (wt %)	0.7	5.9	7	8.5
Char in air at 700° C. (wt %)	0.1	0.1	0.1	0.1
Char in air at 800° C. (wt %)	0.1	0.1	0.1	0.1
M_n(amu)	16014	15219	20889	14438
M_w(amu)	134721	128710	230010	167610

Additional characterization of Comparative Example B and Examples 15-17 is summarized in Table 16. In the solvent resistance test with methyl ethyl ketone (MEK), samples for Comparative Example B and Example 15 completely dissolved, the sample for Example 16 partially dissolved and lost its structural integrity, and the sample for Example 17 gained weight, presumably by absorbing solvent. Further observations include:

- The glass transition temperature increased with thermoplastic polyurethanes containing the residue of hydroxy-diterminated poly(phenylene ether);
- Coefficient of thermal expansion of Comparative Example B and Example 17 were similar below their respective glass transition temperatures, however, the coefficient of thermal expansion of Example 17 was lower above its glass transition temperature compared to Comparative Example B;
- Oxidative resistance properties (7 days aging at 100° C.) of the thermoplastic polyurethanes containing the residue of hydroxy-diterminated poly(phenylene ether) exceeded those of Comparative Example B;
- Solvent resistance in polar and non-polar media improved with increasing levels of hydroxy-diterminated poly(phenylene ether);
- Resistance to strong base and strong acid was improved with increasing levels of hydroxy-diterminated poly(phenylene ether);
- Dielectric constant and dissipation factor (loss tangent) decreased with increasing levels of hydroxy-diterminated poly(phenylene ether);
- Water absorption decreased with increasing levels of hydroxy-diterminated poly(phenylene ether).

TABLE 16

C. Ex. B	Ex. 15	Ex. 16	Ex. 17

T_gby TMA (° C.)	−40.5	−33	−28	−14
CTE by TMA
Below T_g(μm/m-° C.)	53.4	ND	ND	59.2
Above T_g, (μm/m-° C.)	363	ND	ND	228
Dielectrical properties
Dielectric Constant at 1 MHz	6.38	5.49	4.75	4.25
Dissipation Factor at 1 MHz	0.124	0.109	0.088	0.071
Oxidative Resistance Test, 100° C., 7 days
Tensile Strength at break, 23° C. (kPa)	Too soft	820	834	1862
	to be
	tested
Elongation at break, 23° C. (%)	Too soft	474	880	453
	to be
	tested
Glass transition temperature via DSC,	−45	−35	−28	−13
(° C.)
Solvent resistance, post-test sample
weight (%) relative to pre-test sample
weight of 100%
Toluene	290	242	201	153
MEK	Dissolved	Dissolved	Dissolved	252
			partially
Hydrochloric Acid, pH 1	84	64	47	19
Sodium hydroxide, pH 13	70	62	47	28
Water absorption. 50° C. and 100% RH for	11.8	7.5	6.2	4.7
7 days, Weight change (%)

Claims

The invention claimed is:

1. A linear thermoplastic polyurethane comprising:

at least three poly(phenylene ether) repeat units having the structure

wherein each occurrence of Q¹is independently halogen, C₁-C₁₂hydrocarbylthio, C₁-C₁₂hydrocarbyloxy, C₂-C₁₂halohydrocarbyloxy wherein at least two carbon atoms separate the halogen and oxygen atoms, or unsubstituted or substituted C₁-C₁₂hydrocarbyl provided that the hydrocarbyl group is not tertiary hydrocarbyl; each occurrence of Q²is independently hydrogen, halogen, C₁-C₁₂hydrocarbylthio, C₁-C₁₂hydrocarbyloxy, C₂-C₁₂halohydrocarbyloxy wherein at least two carbon atoms separate the halogen and oxygen atoms, or unsubstituted or substituted C₁-C₁₂hydrocarbyl provided that the hydrocarbyl group is not tertiary hydrocarbyl; each occurrence of R¹and R²is independently hydrogen, halogen, C₁-C₁₂hydrocarbylthio, hydrocarbyloxy, C₂-C₁₂halohydrocarbyloxy wherein at least two carbon atoms separate the halogen and oxygen atoms, or unsubstituted or substituted C₁-C₁₂hydrocarbyl provided that the hydrocarbyl group is not tertiary hydrocarbyl; m and n are independently 0 to 20, provided that the sum of m and n is at least 3; and Y is selected from

wherein each occurrence of R³-R⁶is independently hydrogen or C₁-C₁₂hydrocarbyl; and

at least three diisocyanate residue repeat units having the structure

wherein R⁷is, independently in each repeat unit, C₄-C₁₈hydrocarbylene;

wherein at least one terminal oxygen atom of each poly(phenylene ether) repeat unit is covalently bonded to a terminal carbamoyl group of a diisocyanate residue repeat unit to form a urethane moiety.

2. The linear thermoplastic polyurethane of claim 1, wherein the poly(phenylene ether) repeat units have the structure

3. The linear thermoplastic polyurethane of claim 1, wherein each diisocyanate residue repeat units independently has a structure selected from

4. The linear thermoplastic polyurethane of claim 1, further comprising at least three diol repeat units, each diol repeat unit comprising the residue of an alkylene diol, an alkylene ether diol, a polyether diol, an alkoxylate of an aromatic diol, or a polyester diol.

5. The linear thermoplastic polyurethane of claim 1, comprising 5 to 95 weight percent of the poly(phenylene ether) repeat units, and 5 to 40 weight percent of the diisocyanate residue repeat units.

6. The linear thermoplastic polyurethane of claim 5, further comprising 5 to 70 weight percent of diol repeat units, each diol repeat unit comprising the residue of an alkylene diol, an alkylene ether diol, a polyether diol, an alkoxylate of an aromatic diol, or a polyester diol.

7. The linear thermoplastic polyurethane of claim 1, having a weight average molecular weight of 10,000 to 250,000 atomic mass units.

8. The linear thermoplastic polyurethane of claim 1,

wherein the poly(phenylene ether) repeat units have the structure

wherein each occurrence of Q⁵and Q⁶is independently methyl or di-n-butylaminomethyl; and each occurrence of a and b is independently 0 to 20, provided that the sum of a and b is at least 3;

wherein the diisocyanate residue repeat units have a structure selected from

and

wherein the linear thermoplastic polyurethane further comprises at least three diol repeat units, each diol repeat unit comprising the residue of an alkylene diol, an alkylene ether diol, a polyether diol, an alkoxylate of an aromatic diol, or a polyester diol.

9. An article comprising a linear thermoplastic polyurethane comprising:

at least three poly(phenylene ether) repeat units having the structure

at least three diisocyanate residue repeat units having the structure

wherein R⁷is, independently in each repeat unit, C₄-C₁₈hydrocarbyl;

10. The article of claim 9, wherein the article is selected from the group consisting of films, cable sheathing, spiral tubing, pneumatic tubing, blow molded bellows, ski boot shells, sport shoe soles, caster tires, automotive body panels, and automotive rocker panels.

11. A method of forming a linear thermoplastic polyurethane, the method comprising:

reacting a hydroxy-diterminated poly(phenylene ether) with an organic diisocyanate to form a linear thermoplastic polyurethane;

wherein the hydroxy-diterminated poly(phenylene ether) has the structure

wherein the organic diisocyanate has the structure

O═C═N—R⁷—N═C═O

wherein R⁷is C₄-C₁₈hydrocarbylene; and

wherein the linear thermoplastic polyurethane comprises at least three poly(phenylene ether) repeat units and at least three diisocyanate residue repeat units.

12. The method of claim 11, comprising reacting the organic diisocyanate with the hydroxy-diterminated poly(phenylene ether) and a diol selected from the group consisting of alkylene diols, alkylene ether diols, polyether diols, alkoxylates of aromatic diols, polyester diols, and combinations thereof.

13. The method of claim 11, wherein said reacting is conducted in the absence of a catalyst.

14. The method of claim 11, wherein said reacting is conducted in the presence of a catalyst.

15. The method of claim 11, wherein said reacting is conducted in the absence of solvent.

16. The method of claim 11,

wherein the hydroxy-diterminated poly(phenylene ether) has the structure

wherein each occurrence of Q⁵and Q⁶is independently methyl or di-n-butylaminomethyl, and each occurrence of a and b is independently 0 to 20, provided that the sum of a and b is at least 3;

wherein the organic diisocyanate is selected from the group consisting of 2,4′-diphenylmethane diisocyanate, 4,4′-diphenylmethane diisocyanate, toluene 2,6-diisocyanate, toluene 2,4-diisocyanate, and combinations thereof; and

wherein the method comprises reacting the organic diisocyanate with the hydroxy-diterminated poly(phenylene ether) and a diol selected from the group consisting of alkylene diols, alkylene ether diols, polyether diols, alkoxylates of aromatic diols, polyester diols, and combinations thereof.